Using zeolite SSZ-59 for reduction of oxides of nitrogen in a gas stream

ABSTRACT

The present invention relates to new crystalline zeolite SSZ-59 and process employing SSZ-59 as a catalyst.

BACKGROUND OF THE INVENTION

1. Field of the Invention

The present invention relates to new crystalline zeolite SSZ-59 and processes employing SSZ-59 as a catalyst.

2. State of the Art

Because of their unique sieving characteristics, as well as their catalytic properties, crystalline molecular sieves and zeolites are especially useful in applications such as hydrocarbon conversion, gas drying and separation. Although many different crystalline molecular sieves have been disclosed, there is a continuing need for new zeolites with desirable properties for gas separation and drying, hydrocarbon and chemical conversions, and other applications. New zeolites may contain novel internal pore architectures, providing enhanced selectivities in these processes.

Crystalline aluminosilicates are usually prepared from aqueous reaction mixtures containing alkali or alkaline earth metal oxides, silica, and alumina. Crystalline borosilicates are usually prepared under similar reaction conditions except that boron is used in place of aluminum. By varying the synthesis conditions and the composition of the reaction mixture, different zeolites can often be formed.

SUMMARY OF THE INVENTION

The present invention is directed to a family of crystalline molecular sieves with unique properties, referred to herein as “zeolite SSZ-59” or simply “SSZ-59”. Preferably, SSZ-59 is obtained in its silicate, aluminosilicate, titanosilicate, vanadosilicate or borosilicate form. The term “silicate” refers to a zeolite having a high mole ratio of silicon oxide relative to aluminum oxide, preferably a mole ratio greater than 100, including zeolites comprised entirely of silicon oxide. As used herein, the term “aluminosilicate” refers to a zeolite containing both alumina and silica and the term “borosilicate” refers to a zeolite containing oxides of both boron and silicon.

In accordance with the present invention there is provided an improved process for the reduction of oxides of nitrogen contained in a gas stream in the presence of oxygen wherein said process comprises contacting the gas stream with a zeolite, the improvement comprising using as the zeolite a zeolite having a mole ratio greater than about 20 of an oxide of a first tetravalent element to an oxide of a second tetravalent element different from said first tetravalent element, trivalent element, pentavalent element or mixture thereof and having, after calcination, the X-ray diffraction lines of Table II. The zeolite may contain a metal or metal ions (such as cobalt, copper or mixtures thereof) capable of catalyzing the reduction of the oxides of nitrogen, and may be conducted in the presence of a stoichiometric excess of oxygen. In a preferred embodiment, the gas stream is the exhaust stream of an internal combustion engine.

DETAILED DESCRIPTION OF THE INVENTION

The present invention comprises a family of crystalline, zeolites designated herein “zeolite SSZ-59” or simply “SSZ-59”. SSZ-59 is believed to be a large pore zeolite. As used herein, the term “large pore” means having an average pore size diameter greater than about 6.0 Angstroms, preferably from about 6.5 Angstroms to about 7.5 Angstroms.

In preparing SSZ-59 zeolites, a N-methyl-N-[(1-phenylcyclopentyl)methyl]heptamethyleneiminium cation, N-methyl-N-[(1-(4-chlorophenyl)cyclopentyl)methyl]heptamethyleneiminium cation, N-methyl-N-[(1-phenylcyclopentyl)methyl]hexamethyleneiminium cation, N-methyl-N-[(1-(4-chlorophenyl)cyclopentyl)methyl]hexamethyleneiminium cation, N-methyl-N-[(1-phenylcyclopentyl)methyl]piperidinium cation or N-methyl-N-[(1-(4-chlorophenyl)cyclopentyl)methyl]piperidinium cation is used as a crystallization template. In general, SSZ-59 is prepared by contacting an active source of one or more oxides selected from the group consisting of monovalent element oxides, divalent element oxides, trivalent element oxides, and tetravalent element oxides with the N-methyl-N-[(1-phenylcyclopentyl)methyl]heptamethyleneiminium cation, N-methyl-N-[(1-(4-chlorophenyl)cyclopentyl)methyl]heptamethyleneiminium cation, N-methyl-N-[(1-phenylcyclopentyl)methyl]hexamethyleneiminium cation N-methyl-N-[(1-(4-chlorophenyl)cyclopentyl)methyl]hexamethyleneiminium cation, N-methyl-N-[(1-phenylcyclopentyl)methyl]piperidinium cation or N-methyl-N-[(1-(4-chlorophenyl)cyclopentyl)methyl]piperidinium cation templating agent.

SSZ-59 is prepared from a reaction mixture having the composition shown in Table A below.

TABLE A Reaction Mixture Typical Preferred YO₂/W_(a)O_(b) >20 35-70 OH—/YO₂ 0.1-0.5 0.15-0.3  Q/YO₂ 0.05-0.5  0.1-0.2 M_(2/n)/YO₂ 0.02-0.04  0.1-0.25 H₂O/YO₂ 20-80 25-40

wherein Y is silicon, germanium or a mixture thereof; W is aluminum, gallium, iron, boron, titanium, indium, vanadium or mixtures thereof; a is 1 or 2, and b is 2 when a is 1 (i.e., W is tetravalent) and b is 3 when a is 2 (i.e., W is trivalent); M is an alkali metal cation, alkaline earth metal cation or mixtures thereof; n is the valence of M (i.e., 1 or 2); and Q is N-methyl-N-[(1-phenylcyclopentyl)methyl]heptamethyleneiminium cation, N-methyl-N-[(1-(4-chlorophenyl)cyclopentyl)methyl]heptamethyleneiminium cation, N-methyl-N-[(1-phenylcyclopentyl)methyl]hexamethyleneiminium cation, N-methyl-N-[(1-(4-chlorophenyl)cyclopentyl)methyl]hexamethyleneiminium cation, N-methyl-N-[(1-phenylcyclopentyl)methyl]piperidinium cation or N-methyl-N-[(1-(4-chlorophenyl)cyclopentyl)methyl]piperidinium cation.

In practice, SSZ-59 is prepared by a process comprising:

(a) preparing an aqueous solution containing sources of at least one oxide capable of forming a crystalline molecular sieve and a N-methyl-N-[(1-phenylcyclopentyl)methyl]heptamethyleneiminium cation, N-methyl-N-[(1-(4-chlorophenyl)cyclopentyl)methyl]heptamethyleneiminium cation, N-methyl-N-[(1-phenylcyclopentyl)methyl]hexamethyleneiminium cation, N-methyl-N-[(1-(4-chlorophenyl)cyclopentyl)methyl]hexamethyleneiminium cation, N-methyl-N-[(1-phenylcyclopentyl)methyl]piperidinium cation or N-methyl-N-[(1-(4-chlorophenyl)cyclopentyl)methyl]piperidinium cation having an anionic counterion which is not detrimental to the formation of SSZ-59;;

(b) maintaining the aqueous solution under conditions sufficient to form crystals of SSZ-59; and

(c) recovering the crystals of SSZ-59.

Accordingly, SSZ-59 may comprise the crystalline material and the templating agent in combination with metallic and non-metallic oxides bonded in tetrahedral coordination through shared oxygen atoms to form a cross-linked three dimensional crystal structure. The metallic and non-metallic oxides comprise one or a combination of oxides of a first tetravalent element(s), and one or a combination of a second tetravalent element(s) different from the first tetravalent element(s), trivalent element(s), pentavalent element(s) or mixture thereof. The first tetravalent element(s) is preferably selected from the group consisting of silicon, germanium and combinations thereof. More preferably, the first tetravalent element is silicon. The second tetravalent element (which is different from the first tetravalent element), trivalent element and pentavalent element is preferably selected from the group consisting of aluminum, gallium, iron, boron, titanium, indium, vanadium and combinations thereof. More preferably, the second trivalent or tetravalent element is aluminum or boron.

Typical sources of aluminum oxide for the reaction mixture include aluminates, alumina, aluminum colloids, aluminum oxide coated on silica sol, hydrated alumina gels such as Al(OH)₃ and aluminum compounds such as AlCl₃ and Al₂(SO₄)₃. Typical sources of silicon oxide include silicates, silica hydrogel, silicic acid, fumed silica, colloidal silica, tetra-alkyl orthosilicates, and silica hydroxides. Boron, as well as gallium, germanium, titanium, indium, vanadium and iron, can be added in forms corresponding to their aluminum and silicon counterparts.

A source zeolite reagent may provide a source of aluminum or boron. In most cases, the source zeolite also provides a source of silica. The source zeolite in its dealuminated or deboronated form may also be used as a source of silica, with additional silicon added using, for example, the conventional sources listed above. Use of a source zeolite reagent as a source of alumina for the present process is more completely described in U.S. Pat. No. 5,225,179, issued Jul. 6, 1993 to Nakagawa entitled “Method of Making Molecular Sieves”, the disclosure of which is incorporated herein by reference.

Typically, an alkali metal hydroxide and/or an alkaline earth metal hydroxide, such as the hydroxide of sodium, potassium, lithium, cesium, rubidium, calcium, and magnesium, is used in the reaction mixture; however, this component can be omitted so long as the equivalent basicity is maintained. The templating agent may be used to provide hydroxide ion. Thus, it may be beneficial to ion exchange, for example, the halide for hydroxide ion, thereby reducing or eliminating the alkali metal hydroxide quantity required. The alkali metal cation or alkaline earth cation may be part of the as-synthesized crystalline oxide material, in order to balance valence electron charges therein.

The reaction mixture is maintained at an elevated temperature until the crystals of the SSZ-59 zeolite are formed. The hydrothermal crystallization is usually conducted under autogenous pressure, at a temperature between 100° C. and 200° C., preferably between 135° C. and 160° C. The crystallization period is typically greater than 1 day and preferably from about 3 days to about 20 days.

Preferably, the zeolite is prepared using mild stirring or agitation.

During the hydrothermal crystallization step, the SSZ-59 crystals can be allowed to nucleate spontaneously from the reaction mixture. The use of SSZ-59 crystals as seed material can be advantageous in decreasing the time necessary for complete crystallization to occur. In addition, seeding can lead to an increased purity of the product obtained by promoting the nucleation and/or formation of SSZ-59 over any undesired phases. When used as seeds, SSZ-59 crystals are added in an amount between 0.1 and 10% of the weight of silica used in the reaction mixture.

Once the zeolite crystals have formed, the solid product is separated from the reaction mixture by standard mechanical separation techniques such as filtration. The crystals are water-washed and then dried, e.g., at 90° C. to 150° C. for from 8 to 24 hours, to obtain the as-synthesized SSZ-59 zeolite crystals. The drying step can be performed at atmospheric pressure or under vacuum.

SSZ-59 as prepared has a mole ratio of an oxide selected from silicon oxide, germanium oxide and mixtures thereof to an oxide selected from aluminum oxide, gallium oxide, iron oxide, boron oxide, titanium oxide, indium oxide, vanadium oxide and mixtures thereof greater than about 20; and has, after calcination, the X-ray diffraction lines of Table II below. SSZ-59 further has a composition, as synthesized (i.e., prior to removal of the templating agent from the zeolite) and in the anhydrous state, in terms of mole ratios, shown in Table B below.

TABLE B As-Synthesized SSZ-59 YO₂/W_(c)O_(d) >20 M_(2/n)/YO₂ 0.01-0.03 Q/YO₂ 0.02-0.05

where Y, W, M, n and Q are as defined above and c is 1 or 2; d is 2 when c is 1 (i.e., W is tetravalent) or d is 3 or 5 when c is 2 (i.e., d is 3 when W is trivalent or 5 when W is pentavalent).

SSZ-59 can be made essentially aluminum free, i.e., having a silica to alumina mole ratio of ∞. A method of increasing the mole ratio of silica to alumina is by using standard acid leaching or chelating treatments. However, essentially aluminum-free SSZ-59 can be synthesized directly using essentially aluminum-free silicon sources as the main tetrahedral metal oxide component, if boron is also present. SSZ-59 can also be prepared directly as either an aluminosilicate or a borosilicate.

Lower silica to alumina ratios may also be obtained -by using methods which insert aluminum into the crystalline framework. For example, aluminum insertion may occur by thermal treatment of the zeolite in combination with an alumina binder or dissolved source of alumina. Such procedures are described in U.S. Pat. No. 4,559,315, issued on Dec. 17, 1985 to Chang et al.

It is believed that SSZ-59 is comprised of a new framework structure or topology which is characterized by its X-ray diffraction pattern. SSZ-59 zeolites, as-synthesized, have a crystalline structure whose X-ray powder diffraction pattern exhibit the characteristic lines shown in Table I and is thereby distinguished from other zeolites.

TABLE I As-Synthesized SSZ-59 2 Theta^((a)) d Relative Intensity^((b)) 6.1 14.5 M 7.2 12.3 S 8.3 10.6 S 14.4 6.14 W 15.7 5.64 W 17.1 5.18 W 18.45 4.80 W 20.75 4.28 VS 22.45 3.96 M 25.3 3.52 M 27.5 3.24 W 35.75 2.51 W ^((a))±0.2 ^((b))The X-ray patterns provided are based on a relative intensity scale in which the strongest line in the X-ray pattern is assigned a value of 100: W(weak) is less than 20; M(medium) is between 20 and 40; S(strong) is between 40 and 60; VS(very strong) is greater than 60.

Table IA below shows the X-ray powder diffraction lines for as-synthesized SSZ-59 including actual relative intensities.

TABLE IA Two Theta^((a)) d-spacing (Å) Intensity I/Io × 100 6.07 14.54 37 7.20 12.26 45 8.28 10.68 55 14.42 6.140 12 15.71 5.638 6 16.72 Sh 5.298 5 17.10 5.181 14 17.93 Sh 4.942 3 18.24 Sh 4.860 9 18.46 4.804 11 19.33 4.589 3 20.75 4.278 100 21.31 Sh 4.165 6 21.95 4.047 7 22.45 3.957 24 22.99 3.866 3 24.76 3.593 10 25.30 3.517 18 25.54 Sh 3.485 14 26.23 3.395 8 27.22 Sh 3.274 7 27.47 3.244 15 29.09 3.067 2 29.67 3.009 3 30.21 2.956 6 31.09 2.875 5 32.17 2.780 6 33.05 2.708 2 33.55 2.669 2 34.48 2.599 4 35.76 2.509 15 37.00 2.427 2 ^((a))±0.2

After calcination, the SSZ-59 zeolites have a crystalline structure whose X-ray powder diffraction pattern include the characteristic lines shown in Table II:

TABLE II Calcined SSZ-59 2 Theta^((a)) d Relative Intensity 6.1 14.5 VS 7.2 12.3 VS 8.3 10.6 VS 15.7 5.64 W 17.1 5.18 M 18.5 4.79 W 20.7 4.29 S 22.4 3.97 W 25.2 3.53 M 27.5 3.24 W 35.6 2.52 W ^((a))±0.2

Table IIA below shows the X-ray powder diffraction lines for calcined SSZ-59 including actual relative intensities.

TABLE IIA Two Theta (deg.)^((a)) d-spacing (Å) Intensity I/Io × 100 6.11 14.46 87 7.20 12.27 74 8.28 10.67 100 10.54 8.391 2 15.69 5.642 5 17.09 5.185 12 18.24 Sh 4.859 5 18.53 4.785 10 19.28 4.600 3 20.71 4.286 65 21.50 Sh 4.129 2 21.90 Sh 4.055 3 22.40 3.966 16 24.11 3.688 2 24.84 Sh 3.581 7 25.24 3.526 20 25.53 Sh 3.486 11 26.20 3.399 4 27.19 Sh 3.277 2 27.53 3.237 7 29.66 3.009 2 30.22 2.955 3 32.14 2.783 3 33.02 2.711 2 34.49 2.599 1 35.64 2.517 9 36.83 2.439 2 37.11 2.421 1 39.56 2.277 1 ^((a))±0.2

The X-ray powder diffraction patterns were determined by standard techniques. The radiation was the K-alpha/doublet of copper. The peak heights and the positions, as a function of 2θ where θ is the Bragg angle, were read from the relative intensities of the peaks, and d, the interplanar spacing in Angstroms corresponding to the recorded lines, can be calculated.

The variation in the scattering angle (two theta) measurements, due to instrument error and to differences between individual samples, is estimated at±0.20 degrees.

The X-ray diffraction pattern of Table I is representative of “as-synthesized” or “as-made” SSZ-59 zeolites. Minor variations in the diffraction pattern can result from variations in the silica-to-alumina or silica-to-boron mole ratio of the particular sample due to changes in lattice constants. In addition, sufficiently small crystals will affect the shape and intensity of peaks, leading to significant peak broadening.

Representative peaks from the X-ray diffraction pattern of calcined SSZ-59 are shown in Table II. Calcination can also result in changes in the intensities of the peaks as compared to patterns of the “as-made” material, as well as minor shifts in the diffraction pattern. The zeolite produced by exchanging the metal or other cations present in the zeolite with various other cations (such as H⁺ or NH₄ ⁺) yields essentially the same diffraction pattern, although again, there may be minor shifts in the interplanar spacing and variations in the relative intensities of the peaks. Notwithstanding these minor perturbations, the basic crystal lattice remains unchanged by these treatments.

Crystalline SSZ-59 can be used as-synthesized, but preferably will be thermally treated (calcined). Usually, it is desirable to remove the alkali metal cation by ion exchange and replace it with hydrogen, ammonium, or any desired metal ion. The zeolite can be leached with chelating agents, e.g., EDTA or dilute acid solutions, to increase the silica to alumina mole ratio. The zeolite can also be steamed; steaming helps stabilize the crystalline lattice to attack from acids.

The zeolite can be used in intimate combination with hydrogenating components, such as tungsten, vanadium molybdenum, rhenium, nickel cobalt, chromium, manganese, or a noble metal, such as palladium or platinum, for those applications in which a hydrogenation-dehydrogenation function is desired.

Metals may also be introduced into the zeolite by replacing some of the cations in the zeolite with metal cations via standard ion exchange techniques (see, for example, U.S. Pat. No. 3,140,249 issued Jul. 7, 1964 to Plank et al.; 3,140,251 issued Jul. 7, 1964 to Plank et al.; and 3,140,253 issued Jul. 7, 1964 to Plank et al.). Typical replacing cations can include metal cations, e.g., rare earth, Group IA, Group IIA and Group VIII metals, as well as their mixtures. Of the replacing metallic cations, cations of metals such as rare earth, Mn, Ca, Mg, Zn, Cd, Pt, Pd, Ni, Co, Ti, Al, Sn, and Fe are particularly preferred.

The hydrogen, ammonium, and metal components can be ion-exchanged into the SSZ-59. The zeolite can also be impregnated with the metals, or, the metals can be physically and intimately admixed with the zeolite using standard methods known to the art.

Typical ion-exchange techniques involve contacting the synthetic zeolite with a solution containing a salt of the desired replacing cation or cations. Although a wide variety of salts can be employed, chlorides and other halides, acetates, nitrates, and sulfates are particularly preferred. The zeolite is usually calcined prior to the ion exchange procedure to remove the organic matter present in the channels and on the surface, since this results in a more effective ion exchange. Representative ion exchange techniques are disclosed in a wide variety of patents including U.S. Pat. No. 3,140,249 issued on Jul. 7, 1964 to Plank et al.; 3,140,251 issued on Jul. 7, 1964 to Plank et al.; and 3,140,253 issued on Jul. 7, 1964 to Plank et al.

Following contact with the salt solution of the desired replacing cation, the zeolite is typically washed with water and dried at temperatures ranging from 65° C. to about 200° C. After washing, the zeolite can be calcined in air or inert gas at temperatures ranging from about 200° C. to about 800° C. for periods of time ranging from 1 to 48 hours, or more, to produce a catalytically active product especially useful in hydrocarbon conversion processes.

Regardless of the cations present in the synthesized form of SSZ-59, the spatial arrangement of the atoms which form the basic crystal lattice of the zeolite remains essentially unchanged.

SSZ-59 can be formed into a wide variety of physical shapes. Generally speaking, the zeolite can be in the form of a powder, a granule, or a molded product, such as extrudate having a particle size sufficient to pass through a 2-mesh (Tyler) screen and be retained on a 400-mesh (Tyler) screen. In cases where the catalyst is molded, such as by extrusion with an organic binder, the aluminosilicate can be extruded before drying, or, dried or partially dried and then extruded.

SSZ-59 can be composited with other materials resistant to the temperatures and other conditions employed in organic conversion processes. Such matrix materials include active and inactive materials and synthetic or naturally occurring zeolites as well as inorganic materials such as clays, silica and metal oxides. Examples of such materials and the manner in which they can be used are disclosed in U.S. Pat. No. 4,910,006, issued May 20, 1990 to Zones et al., and U.S. Pat. No. 5,316,753, issued May 31, 1994 to Nakagawa, both of which are incorporated by reference herein in their entirety.

SSZ-59 may be used for the catalytic reduction of the oxides of nitrogen in a gas stream. Typically, the gas stream also contains oxygen, often a stoichiometric excess thereof. Also, the SSZ-59 may contain a metal or metal ions within or on it which are capable of catalyzing the reduction of the nitrogen oxides. Examples of such metals or metal ions include copper, cobalt and mixtures thereof.

One example of such a process for the catalytic reduction of oxides of nitrogen in the presence of a zeolite is disclosed in U.S. Pat. No. 4,297,328, issued Oct. 27, 1981 to Ritscher et al., which is incorporated by reference herein. There, the catalytic process is the combustion of carbon monoxide and hydrocarbons and the catalytic reduction of the oxides of nitrogen contained in a gas stream, such as the exhaust gas from an internal combustion engine. The zeolite used is metal ion-exchanged, doped or loaded sufficiently so as to provide an effective amount of catalytic copper metal or copper ions within or on the zeolite. In addition, the process is conducted in an excess of oxidant, e.g., oxygen.

EXAMPLES

The following examples demonstrate but do not limit the present invention. The templating agents indicated in Table C below are used in these examples.

TABLE C N-Methyl-N-[(1-phenylcyclopenyl)methyl]piperidinium

N-Methyl-N-[(1-(4-chlorophenyl)cyclopehnyl)methyl]piperidinium cation

N-Methyl-N-[(1-phenylcyclopenyl)methyl]heptamethyleneiminium cation

N-Methyl-N[(1-(4-chlorophenyl)cyclopentyl)methyl]heptamethylene- iminium cation

N-Methyl-N[(1-phenylcyclopentyl)methyl]hexamethyleneiminium cation

N-Methyl-N-[(1-(4-chlorophenyl)cyclopentyl)methyl]hexamethylene- iminium cation

The anion (X⁻) associated with the cation may be any anion which is not detrimental to the formation of the zeolite. Representative anions include halogen, e.g., fluoride, chloride, bromide and iodide, hydroxide, acetate, sulfate, tetrafluoroborate, carboxylate, and the like. Hydroxide is the most preferred anion.

Example 1 Synthesis of N-methyl-N-[(1-phenylcyclopentyl)methyl]piperidinium cation (Template A)

The templating agent was synthesized from the commercially available starting materials according to the synthetic sequence scheme shown below.

Synthesis of the starting amide(phenylcyclopentyl piperidyl ketone)

To a mechanically stirred solution of piperidine (85.15 gm; 1 mole) and triethylamine (126.5 gm; 1.25 mole) in 800 ml anhydrous benzene in a 2-liter three-neck round bottom reaction a 215 gm (1.03 mole) of 1-phenylcyclopentanecarbonyl chloride (synthesis of this compound is described below), dissolved in 100 ml benzene, were added drop wise via an addition funnel at 0° C. over a period of 20 minutes. The resulting mixture (a solution with tan-colored solids) was allowed to gradually warm up to room temperature and continued to stir over night. The resulting Mixture was transferred to a 2-liter separatory funnel and diluted with 600 ml ethyl acetate. The mixture was washed three times with water (300 ml each) and once with 300 ml saturated sodium chloride solution. The organic phase was dried over anhydrous magnesium sulfate, filtered and concentrated at reduced pressure on a rotary evaporator to give 241 gm of the desired amide (pure by NMR analysis) as a tan-colored solid.

Reduction of phenylcyclopentyl piperidyl ketone to the corresponding N-[(1-phenylcyclopentyl)methyl]piperidine

To a mechanically stirred suspension of lithium aluminum hydride (37.95 gm; 1 mole) in 1000 ml anhydrous tetrahydrofuran (THF) at 0° C. (ice-water bath) in a 2-liter 3-neck flask, the amide (128.7 gm, 0.5 mole) dissolved in 200 ml anhydrous THF was added drop-wise via an addition funnel. Once the addition was completed, the ice-water bath was removed and the reaction was stirred for 0.5 hrs at room temperature. The reaction was, then, heated at reflux for 3 hrs. The heat source was removed and once the reaction mixture cooled down to room temperature, the mixture was cooled to 0° C. by means of an ice-water bath. The mixture was diluted with 500 ml ethyl ether and the reaction was worked up by adding 225 ml of 15% aqueous NaOH solution drop-wise via an addition funnel. The resulting bi-phasic (colorless liquid and white precipitate) solution was filtered though a fritted-glass funnel. The filtrate was dried over anhydrous magnesium sulfate, filtered and concentrated at reduced pressure on a rotary evaporator to give 118 gm of the desired amine (pure by NMR analysis) as a pale yellow oil.

Quaternization (synthesis of N-methyl-N-[(1-phenylcyclopentyl)methyl]piperidinium iodide)

To a mechanically stirred solution of [(1-phenylcyclopentyl)methyl]piperidine (115 gm; 0.47 mole) in 1000 ml methanol (ACS reagent), methyl iodide (100 gm; 0.7 mole) were added. The resulting mixture was stirred for 48 hrs. Then an additional 35 gm (0.5 mole equivalent) of methyl iodide was added and the reaction was heated for 1 hr. The resulting solution was concentrated under reduced pressure on a rotary evaporator to give 175 gm of a tan solid material. The obtained solid was re-crystallized by dissolving in hot isopropyl alcohol and allowed to re-crystallize overnight. Re-crystallization afforded 171 gm of the product (NMR analysis) as shinny white needles.

Ion Exchange (making N-methyl-N-[(1-phenylcyclopentyl)methyl]piperidinium hydroxide)

To a gently stirred solution of 100 gm (0.26 mole) of methyl(((phenyl)cyclopentyl)methyl)piperidinium iodide in 400 ml de-ionized water in a plastic bottle, 325 gm of Ion-Exchange Resin-OH (BIO RAD®) were added and the mixture was let to stir at room temperature overnight. The mixture was filtered through a fritted-glass funnel and the solids were rinsed with additional 75 ml of water. A small aliquot from the filtrate was titrated with 0.1 N HCl to indicate a total yield of 0.22 mole of OH ions (hence 0.22 of N-methyl-N-[(1-phenylcyclopentyl)methyl]piperidinium hydroxide).

Synthesis of 1-phenylcyclopentanecarbonyl chloride

The carboxylic acid chlorides used in the synthesis of the parent amides were all synthesized as described below. In a 1-liter 3-neck flask, 200 gm (1.05 mole) of 1-phenylcyclopentanecarboxylic acid (ACROS ORGANICS) was added drop-wise to stirring excess of thionyl chloride (Aldrich) under nitrogen. The resulting mixture was heated at reflux for two hrs. The reaction was further stirred at room temperature overnight. The resulting brown-red solution was concentrated at reduced pressure and heat on a rotary evaporator to remove excess thionyl chloride. The reaction yielded 216 gm in of a lachrymator substance whose ¹H-NMR and ¹³C-NMR spectra were ideal for the desired acid chloride.

Example 2 Synthesis of templating agent N-methyl-N-[(1-(4-chlorophenyl)cyclopentyl)methyl]piperidinium cation (Template B)

N-methyl-N-[(1-(4-chlorophenyl)cyclopentyl)methyl]piperidinium cation was synthesized using the above procedure starting from piperidine and 1-(4-chlorophenyl)cyclopentanecarbonyl chloride.

Example 3 Synthesis of templating agent N-methyl-N-[(1-phenylcyclopentyl)methyl]heptamethyleneiminium cation (Template C)

N-methyl-N-[(1-phenyl)cyclopentyl)methyl]heptamethyleneiminium cation was synthesized using the above procedure starting from heptametheleneimine and 1-phenylcyclopentanecarbonyl chloride

Example 4 Synthesis of N-methyl-N-[(1-(4-chlorophenyl)cyclopentyl)methyl]heptamethyleneiminium cation (Template D)

N-methyl-N-[(1-(4-chlorophenyl)cyclopentyl)methyl]heptamethyleneiminium cation was synthesized using the above procedure starting from heptametheleneimine and 1-(4-chlorophenyl)cyclopentanecarbonyl chloride.

Example 5 Synthesis of templating agent N-methyl-N-[(1-phenylcyclopentyl)methyl]hexamethyleneiminium cation (Template E)

N-methyl-N-[(1-phenylcyclopentyl)methyl]hexamethyleneiminium cation was synthesized using the above procedure starting from hexametheleneimine and 1-phenylcyclopentanecarbonyl chloride

Example 6 Synthesis of N-meth yl-N-[(1-(4-chlorophenyl)cyclopentyl)methyl]hexamethyleneiminium cation (Template F)

N-methyl-N-[(1-(4-chlorophenyl)cyclopentyl)methyl]hexamethyleneiminium cation was synthesized using the above procedure starting from hexametheleneimine and 1-(4-chlorophenyl)cyclopentanecarbonyl chloride

Example 7 Synthesis of Boron-SSZ-59

In a 23-cc Teflon liner, 6.48 gm of 0.46 M solution (aqueous) of the templating agent N-methyl-N-[(phenylcyclopentyl)methyl]piperidinium hydroxide (Template A, 3 mmol) were mixed with 1.2 gm of 1.0N NaOH (1.2 mmol) and 4.3 gm of de-ionized water. To this mixture, 0.06 gm of sodium borate decahydrate were added and stirred until completely dissolved. To this mixture, 0.9 gm of CAB-O-SIL M-5 (˜14.7 mmol SiO₂) were added. The mixture was thoroughly stirred and the resulting gel was capped off and placed in steel Parr autoclave and heated in an oven at 160° C. while tumbling at 43 rpm. The progress of the reaction was monitored by Scanning Electron Microscopy at intervals of 6 days. Once completed (after heating for 12 days), the pasty reaction mixture was filtered through a fritted glass funnel. The collected solid was rinsed with water (1 liter) and air-dried overnight. The solids were further dried in an oven at 120° C. for 2 hrs. The reaction yielded 0.9 gm of SSZ-59 as a white powder.

Table IVA below shows the synthesis of Boron-SSZ-59 at varying SiO2/B203 ratios. The data presented in Table IVA is obtained from attempts at making the borosilicate version of SSZ-59 at differentSiO2/B203 ratios while keeping SiO2 to other reagent constant using Template A as structure directing agent.

TABLE IVA* SiO₂/B₂O₃ XRD Results 0 Layered 280 Cristobalite 140 SSZ-59 93.3 SSZ-59 70 SSZ-59 56 SSZ-59 46.7 SSZ-59 40 SSZ-59 35 SSZ-59 31 SSZ-59 28 SSZ-59 25.5 SSZ-59 23.5 SSZ-59 20 SSZ-59 18.7 SSZ-59 15.6 SSZ-59 14 SSZ-59, Cristobalite *SiO₂/OH for all runs was 3.5; H₂O/SiO₂ for all runs was 44

The XRD data appears in Table III below.

TABLE III Two Theta^((a)) d-spacing (Å) Intensity I/Io × 100 6.07 14.54 37 7.20 12.26 45 8.28 10.68 55 14.42 6.140 12 15.71 5.638 6 16.72 Sh 5.298 5 17.10 5.181 14 17.93 Sh 4.942 3 18.24 Sh 4.860 9 18.46 4.804 11 19.33 4.589 3 20.75 4.278 100 21.31 Sh 4.165 6 21.95 4.047 7 22.45 3.957 24 22.99 3.866 3 24.76 3.593 10 25.30 3.517 18 25.54 Sh 3.485 14 26.23 3.395 8 27.22 Sh 3.274 7 27.47 3.244 15 29.09 3.067 2 29.67 3.009 3 30.21 2.956 6 31.09 2.875 5 32.17 2.780 6 33.05 2.708 2 33.55 2.669 2 34.48 2.599 4 35.76 2.509 15 37.00 2.427 2 ^((a))±0.2

Example 8 Synthesis of Aluminum-SSZ-59

In a 23-cc Teflon liner, 6.75 gm of 0.34 M solution (aqueous) of the templating agent N-methyl-N-[(1-phenylcyclopentyl)methyl]heptamethyleneiminium hydroxide (Template C, 2.25 mmol) were mixed with 1.5 gm of 1.0N NaOH (1.5 mmol). To this mixture, 0.25 gm of Union Carbide's LZ-Y52 zeolite were added. Then, 0.8 gm of CAB-O-SIL M-5 (˜13 mmol SiO₂) were added. The mixture was thoroughly stirred and the resulting gel was capped off and placed in steel Parr autoclave and heated in an oven at 160° C. while tumbling at 43 rpm. The progress of the reaction was monitored by Scanning Electron Microscopy at intervals of 6 days. Once completed (after heating for 6 days), the pasty looking reaction mixture was filtered through a fritted glass funnel. The collected solid was rinsed with water (1 liter) and air-dried overnight. The solids were further dried in an oven at 120° C. for 2 hrs. The reaction yielded 0.75 gm of SSZ-59 as a white powder. Analysis by XRD shows the product to be SSZ-59.

SSZ-59 is made in a similar manner using in turn Templates B, D, E and F as the templating agent.

Example 9 Calcination of SSZ-59

The material from Example 8 is calcined in the following manner. A thin bed of material is heated in a muffle furnace from room temperature to 120° C. at a rate of 1° C. per minute and held at 120° C. for three hours. The temperature is then ramped up to 540° C. at the same rate and held at this temperature for 5 hours, after which it is increased to 594° C. and held there for another 5 hours. A 50/50 mixture of air and nitrogen is passed over the zeolite at a rate of 20 standard cubic feet per minute during heating. The X-ray diffraction data for the product is provided in Table IV below.

TABLE IV Two Theta (deg.)^((a)) d-spacing (Å) Intensity I/Io × 100 6.11 14.46 87 7.20 12.27 74 8.28 10.67 100 10.54 8.391 2 15.69 5.642 5 17.09 5.185 12 18.24 Sh 4.859 5 18.53 4.785 10 19.28 4.600 3 20.71 4.286 65 21.50 Sh 4.129 2 21.90 Sh 4.055 3 22.40 3.966 16 24.11 3.688 2 24.84 Sh 3.581 7 25.24 3.526 20 25.53 Sh 3.486 11 26.20 3.399 4 27.19 Sh 3.277 2 27.53 3.237 7 29.66 3.009 2 30.22 2.955 3 32.14 2.783 3 33.02 2.711 2 34.49 2.599 1 35.64 2.517 9 36.83 2.439 2 37.11 2.421 1 39.56 2.277 1 ^((a))±0.2

Example 10 NH₄ Exchange

Ion exchange of calcined SSZ-59 material (prepared in Example 8) is performed using NH₄NO₃ to convert the zeolite from its Na⁺ form to the NH₄ ⁺ form, and, ultimately, the H⁺ form. Typically, the same mass of NH₄NO₃ as zeolite is slurried in water at a ratio of 25-50:1 water to zeolite. The exchange solution is heated at 95° C. for 2 hours and then filtered. This procedure can be repeated up to three times. Following the final exchange, the zeolite is washed several times with water and dried. This NH₄ ⁺ form of SSZ-59 can then be converted to the H⁺ form by calcination (as described in Example 9) to 540° C.

Example 11 Constraint Index Determination

The hydrogen form of the zeolite of Example 8 (after treatment according to Examples 9 and 10) is pelletized at 2-3 KPSI, crushed and meshed to 20-40, and then>0.50 gram is calcined at about 540° C. in air for four hours and cooled in a desiccator. 0.50 Gram is packed into a ⅜ inch stainless steel tube with alundum on both sides of the zeolite bed. A Lindburg furnace is used to heat the reactor tube. Helium is introduced into the reactor tube at 10 cc/min. and at atmospheric pressure. The reactor is heated to about 315° C., and a 50/50 (w/w) feed of n-hexane and 3-methylpentane is introduced into the reactor at a rate of 8 μl/min. Feed delivery is made via a Brownlee pump. Direct sampling into a gas chromatograph begins after 10 minutes of feed introduction. The Constraint Index value is calculated from the gas chromatographic data using methods known in the art, and is found to be 0.27, which suggests a large pore zeolite. At 315° C. and 10 minutes on stream, feed conversion was greater than 62%. SSZ-59 has a very high cracking activity, indicative of strongly acidic sites.

Example 12 Hydrocracking of n-Hexadecane

A sample of SSZ-59 as prepared in Example 8 was treated as in Examples 9 and 10. Then a sample was slurried in water and the pH of the slurry was adjusted to a pH of ˜10 with dilute ammonium hydroxide. To the slurry was added a solution of Pd(NH₃)₄(NO₃)₂ at a concentration which would provide 0.5 wt. % Pd with respect to the dry weight of the zeolite sample. This slurry was stirred for 48 hours at 100° C. After cooling, the slurry was filtered through a glass frit, washed with de-ionized water, and dried at 100° C. The catalyst was then calcined slowly up to 900° F. in air and held there for three hours.

The calcined catalyst was pelletized in a Carver Press and crushed to yield particles with a {fraction (20/40)} mesh size range. Sized catalyst (0.5 g) was packed into a ¼″ OD tubing reactor in a micro unit for n-hexadecane hydroconversion. Table VIII gives the run conditions and the products data for the hydrocracking test on n-hexadecane. After the catalyst was tested with n-hexadecane, it was titrated using a solution of butyl amine in hexane. The temperature was increased and the conversion and product data evaluated again under titrated conditions. The results shown in Table V show that SSZ-59 is effective as a hydrocracking catalyst.

TABLE V Temperature 580° F. WHSV 1.55 PSIG 1200 Titrated? No n-16, % Conversion 94.1 Hydrocracking Conversion, % 72.0 Isomerization Selectivity, % 23.4 C₄ ⁻, % 11.9 C₅ + C₆ % 22.7 C4 i/n 3.14 C5 i/n 4.21 C6 i/n 3.97 C7 i/n 5.07 C8 i/n 6.11 C9 i/n 5.85 C10 i/n 6.12 C11 i/n 4.96 C12 i/n 5.47 

What is claimed is:
 1. In a process for the reduction of oxides of nitrogen contained in a gas stream in the presence of oxygen wherein said process comprises contacting the gas stream with a zeolite, the improvement comprising using as the zeolite a zeolite having a mole ratio greater than about 20 of an oxide of a first tetravalent element to an oxide of a second tetravalent element which is different from said first tetravalent element, trivalent element, pentavalent element or mixture thereof and having, after calcination, the X-ray diffraction lines of Table II.
 2. The process of claim 1 wherein said zeolite contains a metal or metal ions capable of catalyzing the reduction of the oxides of nitrogen.
 3. The process of claim 2 wherein the metal is copper, cobalt or mixtures thereof.
 4. The process of claim 2 wherein the gas stream is the exhaust stream of an internal combustion engine. 